US4578256A - Process for removal of poisonous gases - Google Patents
Process for removal of poisonous gases Download PDFInfo
- Publication number
- US4578256A US4578256A US06/653,093 US65309384A US4578256A US 4578256 A US4578256 A US 4578256A US 65309384 A US65309384 A US 65309384A US 4578256 A US4578256 A US 4578256A
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- United States
- Prior art keywords
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- present
- activated carbon
- iodine
- adsorbent
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
Definitions
- This invention relates to a process of treating poisonous gases containing hydrides of B, P, As, Sb and Se.
- Hydrides such as B 2 H 6 , PH 3 , AsH 3 , SbH 3 and H 2 Se, are utilized in large quantities for raw material gases for production of semiconductors, fumigation gases, etc., but even in trace amounts, are extremely poisonous to the human body. Therefore, the development of a method capable of efficiently removing these hydrides in gas is strongly demanded.
- the present inventors in view of these circumstances, conducted intensive investigation, and as a result, found that by using activated carbon with iodine, iodine compounds and sulfates and nitrates of NH 4 , Ag, Al, Ti, V, Cr, Mn, Fe, Co, Ni, Cu, Zn, Cd, Pb and Sn, supported thereon hydrides of B, P, As, Sb and Se in gases can be removed highly efficiently, which has culminated in the present invention.
- a process of removing one or more kinds of hydrides of As, B, P, Sb or Se from a gas containing one or more kinds of hydrides of As, B, P, Sb or Se which comprises contacting said gas with an adsorbent comprising activated carbon having (1) iodine and/or one or more kinds of iodine compounds (hereinafter referred to in some instances as "First Component") and/or (2) one or more kinds of sulfates and nitrates of NH 4 , Ag, Al, Ti, V, Cr, Mn, Fe, Co, Ni, Cu, Zn, Cd, Pb and Sn (hereinafter referred to in some instances as "Second Component") supported thereon.
- an adsorbent comprising activated carbon having (1) iodine and/or one or more kinds of iodine compounds (hereinafter referred to in some instances as "First Component”) and/or (2) one or more kinds of sulfates and nitrate
- the activated carbon which is useful in the present invention may be any type of activated carbon produced by the known processes from coal, coke, wood charcoal, coconut shells, resins, etc., while its specific surface area is preferably within the range from 200 to 2000 m 2 /g. With reference to its shape and form, use is suitably made for example of spherical- and cylindrical-formed, crushed, powdered and fibrous-formed activated carbon according to the type of gas treatment methods.
- the First Component useful in the present invention include iodides, such as LiI, NaI, KI, RbI, CsI, BeI 2 , MgI 2 , CaI 2 , SrI 2 , BaI 2 , NH 4 I and HI, iodic acid and its salts, such as HIO 3 , NH 4 IO 3 , NaIO 3 and KIO 3 , periodic acid and its salts, such as HIO 4 , NH 4 IO 4 , NaIO 4 and KIO 4 , and iodine oxides, such as I 2 O 5 and IO 2 .
- iodides such as LiI, NaI, KI, RbI, CsI, BeI 2 , MgI 2 , CaI 2 , SrI 2 , BaI 2 , NH 4 I and HI
- iodic acid and its salts such as HIO 3 , NH 4 IO 3 , NaIO 3 and KIO 3
- Second Component which is utilizable, include (NH 4 ) 2 SO 4 , Ag 2 SO 4 , Al 2 (SO 4 ) 3 , Ti 2 (SO 4 ) 3 , VOSO 4 , Cr 2 (SO 4 ) 3 , MnSO 4 , FeSO 4 , Fe 2 (SO 4 ) 3 , CoSO 4 , NiSO 4 , CuSO 4 , ZnSO 4 , CdSO 4 , PbSO 4 , SnSO 4 , NH 4 NO 3 , AgNO 3 , Al(NO 3 ) 3 , Cr(NO 3 ) 3 , Mn(NO 3 ) 2 , Fe(NO 3 ) 2 , Fe(NO 3 ) 3 , Co(NO 3 ) 2 , Ni(NO 3 ) 2 , Cu(NO 3 ) 2 , Zn(NO 3 ) 2 , Cd(NO 3 ) 2 , Pb(NO 3 ) 2 , etc.
- the adsorbent used in the present invention which comprises activated carbon having each of the components being supported thereon, can be produced by impregnating or spraying activated carbon with a solution or suspension of the individual components in water (inclusive of aqueous acid or alkali solutions) or various solvents (e.g., alcohols, such as methanol and ethanol, ketones, such as acetone and methyl ethyl ketone, etc.), and if necessary, by drying the impregnated or sprayed activated carbon at a temperature of not higher than about 130° C. or calcining at a temperature of not lower than 130° C.
- water inclusive of aqueous acid or alkali solutions
- various solvents e.g., alcohols, such as methanol and ethanol, ketones, such as acetone and methyl ethyl ketone, etc.
- the components may be supported simultaneously or may be supported individually, whereby they may be supported in arbitrary order.
- the supported amounts of each of the First and Second Components in activated carbon are 1 mg to 500 mg per g of activated carbon (0.5 mg to 250 mg for silver sulfate and silver nitrate), preferably 5 to 400 mg (1 to 150 mg for silver sulfate and silver nitrate).
- the present invention is usually carried out by contacting a gas containing hydrides of B, P, As, Sb and Se with the adsorbent in the presence of oxygen.
- the contact temperature is not higher than 150° C., preferably -10° to 120° C., more preferably 0° to 100° C., and the contact pressure is not more than 10 atm., preferably 0.01 to 5 atm., with the contact time being 1/20 to 100 seconds as converted at 25° C. and 1 atm., preferably 1/10 to 50 seconds.
- oxygen is not contained in the gas to be treated, it is preferable to add oxygen to the gas.
- the amount of oxygen contained in the gas is usually not less than one mol per mol of hydrides of B, P, As, Sb and Se, preferably not less than 2 mol.
- the contacting of the adsorbent with a gas containing hydrides of B, P, As, Sb and Se can be conducted for example by use of fixed bed, moving bed and fluidized bed.
- Activated carbon A 0 of 16 to 24 mesh having a BET specific surface area of 1,150 m 2 /g was sprayed uniformly with aqueous solutions or suspensions of the required amounts of iodine, iodine compounds and/or sulfates and nitrates of NH 4 , Ag, Al, Ti, V, Cr, Mn, Fe, Co, Ni, Cu, Zn, Cd, Pb and Sn, and then dried at 110° C.
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- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Catalysts (AREA)
Abstract
Description
TABLE 1 __________________________________________________________________________ The first The second Percent removal of AsH.sub.3 Percent removal of PH.sub.3 component and component and at the elapsed time at the elapsed time shown Adsorbent its amount its amount shown below (%) below (%) No. (mg/g) (mg/g) 5 hrs. 10 hrs. 30 hrs. 5 hrs. 10 hrs. 30 hrs. __________________________________________________________________________ A.sub.0 (Control) 0 0 35 5 0 4 0 0 A.sub.1 (The present LiI-50 0 100 85 68 93 61 40 invention) A.sub.2 (The present NaI-50 0 100 88 70 91 65 47 invention) A.sub.3 (The present KI-50 0 100 100 100 100 100 100 invention) A.sub.4 (The present MgI.sub.2 -50 0 100 80 64 98 61 35 invention) A.sub.5 (The present BaI.sub.2 -50 0 100 85 73 90 65 41 invention) A.sub.6 (The present NH.sub.4 I-50 0 100 100 96 95 90 80 invention) A.sub.7 (The present NaIO.sub.3 -50 0 100 100 100 100 85 64 invention) A.sub.8 (The present KIO.sub.3 -50 0 100 100 100 100 100 100 invention) A.sub.9 (The present I.sub.2 -50 0 100 100 100 100 100 100 invention) A.sub.10 (The present I.sub.2 O.sub.5 -50 0 100 100 100 100 100 100 invention) A.sub.11 (The present HIO.sub.3 -50 0 100 100 100 100 100 98 invention) A.sub.12 (The present KI-5 0 90 85 61 88 71 50 invention) A.sub.13 (The present KI-25 0 100 100 100 100 100 90 invention) A.sub.14 (The present KI-400 0 100 100 100 100 100 100 invention) B.sub.1 (The present 0 (NH.sub.4).sub.2 SO.sub.4 -50 96 93 84 90 85 60 invention) B.sub.2 (The present 0 AgNO.sub.3 -5 100 98 90 98 85 53 invention) B.sub.3 (The present 0 Al(NO.sub.3).sub.3 -50 85 60 30 82 60 48 invention) B.sub.4 (The present 0 Ti.sub.2 (SO.sub.4).sub.3 -50 81 48 23 80 55 31 invention) B.sub.5 (The present 0 VOSO.sub.4 -50 98 83 53 87 65 43 invention) B.sub.6 (The present 0 Cr(NO.sub.3).sub.3 -50 88 65 43 75 50 32 invention) B.sub.7 (The present 0 MnSO.sub.4 -50 98 85 61 83 45 21 invention) B.sub.8 (The present 0 FeSO.sub.4 -50 100 100 95 92 80 65 invention) B.sub.9 (The present 0 Fe(NO.sub.3).sub.3 -50 100 100 91 100 90 75 invention) B.sub.10 (The present 0 CoSO.sub.4 -50 98 85 73 85 72 60 invention) B.sub.11 (The present 0 Ni(NO.sub.3).sub.2 -50 95 60 35 83 65 53 invention) B.sub.12 (The present 0 CuSO.sub.4 -50 100 98 71 93 82 61 invention) B.sub.13 (The present 0 Zn(NO.sub.3).sub.2 -50 95 80 63 83 60 46 invention) B.sub.14 (The present 0 CdSO.sub.4 -50 97 78 68 80 64 41 invention) B.sub.15 (The present 0 Pb(NO.sub.3).sub.2 -50 98 83 60 93 72 51 invention) B.sub.16 (The present 0 SnSO.sub.4 -50 100 95 70 95 68 43 invention) B.sub.17 (The present 0 Fe.sub.2 (SO.sub.4).sub.3 -50 100 95 90 100 75 47 invention) __________________________________________________________________________ The first The second Percent removal of AsH.sub.3 Percent removal of PH.sub.3 component and component and at the elapsed time shown at the elapsed time shown Adsorbent its amount its amount below (%) below (%) No. (mg/g) (mg/g) 50 hrs. 100 hrs. 200 hrs. 50 hrs. 100 hrs. 200 hrs __________________________________________________________________________ C.sub.1 (The present NaI-50 AgNO.sub.3 -50 100 100 100 100 100 100 invention) C.sub.2 (The present KI-50 Ti.sub.2 (SO.sub.4).sub.3 -50 100 100 85 100 98 79 invention) C.sub.3 (The present MgI-50 Cr(NO.sub.3).sub.3 -50 100 98 90 100 83 70 invention) C.sub.4 (The present I.sub.2 O.sub.5 -50 Co(NO.sub.3).sub.2 -50 100 100 100 100 100 100 invention) C.sub.5 (The present NH.sub.4 I-50 SnSO.sub.4 -50 100 100 85 100 100 81 invention) C.sub.6 (The present KI-50 Ag.sub.2 SO.sub.4 -5 100 100 88 100 100 100 invention) C.sub.7 (The present KI-50 VOSO.sub.4 -50 100 100 100 100 100 100 invention) C.sub.8 (The present KI-50 Cr.sub.2 (SO.sub.4).sub.3 -50 100 100 100 100 100 100 invention) C.sub.9 (The present KI-50 Mn(NO.sub.3).sub.2 -50 100 100 100 100 100 100 invention) C.sub.10 (The present KI-50 Fe(NO.sub.3).sub.2 -50 100 100 100 100 100 100 invention) C.sub.11 (The present KI-50 Co(NO.sub.3).sub.2 -50 100 100 100 100 100 100 invention) C.sub.12 (The present KI-50 Cu(NO.sub.3).sub.2 -50 100 100 100 100 100 100 invention) C.sub.13 (The present KI-50 ZnSO.sub.4 -50 100 100 100 100 100 100 invention) C.sub.14 (The present NH.sub.4 I-50 FeSO.sub.4 -50 100 100 100 100 100 100 invention) C.sub.15 (The present BaI-50 FeSO.sub.4 -50 100 100 80 100 100 89 invention) C.sub.16 (The present I.sub.2 -5 FeSO.sub.4 -10 100 100 100 100 100 100 invention) KI-10 C.sub.17 (The present I.sub.2 -5 FeSO.sub.4 -10 100 100 100 100 100 100 invention) NH.sub.4 I-10 D.sub.1 (The present KI-5 FeSO.sub.4 -50 100 98 65 100 88 60 invention) D.sub.2 (The present KI-10 FeSO.sub.4 -50 100 100 79 100 100 81 invention) D.sub.3 (The present KI-50 FeSO.sub.4 -50 100 100 100 100 100 100 invention) D.sub.4 (The present KI-50 FeSO.sub.4 -5 100 100 83 100 100 84 invention) D.sub.5 (The present KI-50 FeSO.sub.4 -10 100 100 100 100 100 100 invention) D.sub.6 (The present KI-5 FeSO.sub.4 -5 100 85 77 100 78 61 invention) D.sub.7 (The present KI-5 Fe.sub.2 (SO.sub.4).sub.3 -50 100 93 81 100 96 86 invention) D.sub.8 (The present KI-10 Fe.sub.2 (SO.sub.4).sub.3 -50 100 100 93 100 100 85 invention) D.sub.9 (The present KI-50 Fe.sub.2 (SO.sub.4).sub.3 -5 100 100 95 100 100 83 invention) D.sub.10 (The present KI-50 Fe.sub.2 (SO.sub.4).sub.3 -10 100 100 98 100 100 100 invention) D.sub.11 (The present KI-5 Fe.sub.2 (SO.sub.4).sub.3 -5 100 93 75 100 90 71 invention) D.sub.12 (The present KI-5 Fe.sub.2 (SO.sub.4).sub.3 -50 100 90 68 100 79 57 invention) D.sub.13 (The present KI-5 FeSO.sub.4 -250 100 95 73 100 88 70 invention) D.sub.14 (The present KI-250 FeSO.sub.4 -5 100 100 100 100 100 100 invention) __________________________________________________________________________
TABLE 2 __________________________________________________________________________ The length of time for which The length of time for which The length of time for which the removal percentages the removal percentages the removal percentages Adsorbent for B.sub.2 H.sub.6 reached 95% for H.sub.2 Se reached 95% for SbH.sub.3 reached __________________________________________________________________________ 95% A.sub.0 (Control) 1/6 1/4 1/3 A.sub.3 (The present 63 41 55 invention) A.sub.6 (The present 43 40 48 invention) A.sub.10 (The present 75 78 80 invention) A.sub.11 (The present 30 28 30 invention) B.sub.2 (The present 19 30 45 invention) B.sub.7 (The present 25 19 24 invention) B.sub.8 (The present 21 20 20 invention) B.sub.11 (The present 28 32 19 invention) C.sub.1 (The present 153 198 185 invention) C.sub.7 (The present 258 250 233 invention) C.sub.12 (The present 218 200 223 invention) C.sub.14 (The present 300 310 305 invention) C.sub.17 (The present 313 300 320 invention) D.sub.3 (The present 355 368 390 invention) D.sub.8 (The present 370 373 398 invention) D.sub.13 (The present 195 210 195 invention) __________________________________________________________________________
Claims (6)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58179870A JPS6071040A (en) | 1983-09-27 | 1983-09-27 | Noxious gas adsorbent |
JP58-179870 | 1983-09-27 |
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US4578256A true US4578256A (en) | 1986-03-25 |
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US06/653,093 Expired - Lifetime US4578256A (en) | 1983-09-27 | 1984-09-21 | Process for removal of poisonous gases |
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JP4639276B2 (en) * | 2003-12-17 | 2011-02-23 | 清水建設株式会社 | Deodorant, method for producing the same, and deodorizer |
KR100701576B1 (en) | 2005-02-22 | 2007-03-29 | 주식회사 에이엔씨아이 | Preparation of a High Functional Active Carbon/fibers by Electroless Silver/Iodine Plating Methods |
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Also Published As
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JPH0424094B2 (en) | 1992-04-24 |
JPS6071040A (en) | 1985-04-22 |
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